• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:

    公开号:SU1787150A3
    申请号:SU884355649
    申请日:1988-05-04
    公开日:1993-01-07
    发明作者:Tibor Alpar；Yanosh Dervari；Erne Shmidt
    申请人:Fakokombinat Sombateli；
    IPC主号:
    专利说明:

    The invention relates to methods for the manufacture of building products from hardening mixtures containing a hydraulic binder, and devices for implementing the method. five
    The goal is to increase productivity when using a COg hardening accelerator, to ensure a local supply of COg.
    Figure 1 shows the device in a schematic longitudinal section; Figure 2. - section a-a in figure 1; in Fig.Z a form of execution of the side wall of the formwork on an enlarged scale; in Fig, 4 view B in Fig.Z; figure 5 is a diagram of gas pressure - path - time; 6-11, the cross-sectional shape of building elements manufactured by the method: FIG. 12 is a diagram of the strengthening of the building element according to FIG. 11.
    The device (figures 1 and 2) contains a vertical formwork 1, a loading funnel 2, a ramming mechanism 3, which consists of a piston 4 moving along a double arrow b with an expanding part and a piston 4 drive (not shown) located on both sides of the piston 4 vertical guides 5 for guiding the piston 4 during its reciprocating motion.
    The cavity 6 of the formwork 1 is limited by vertically 30 caliao located at a distance a (see Fig. 1) from each other by walls 7 and 8 with a width S (see Fig. 2), as well as perpendicular and narrow, also vertically located (not shown ) walls. 35 The device (Figs. 1 and 2) serves for the manufacture of building panels 9 with a thickness a, the width of which, perpendicular to the plane of the drawing (see, Fig. 1), is determined by the indicated value S of the slabs 7 and 8, measured in the width direction, while the other the size of the building panel in the plane of the drawing (see Fig. 1), for example, its length, can be chosen any within practical limits, which will be explained below. Formwork 1 is open on the upper and lower sides and has, respectively, a loading opening '10 and an outlet opening 11. The loading funnel 2 enters its lower part into the upper open end of the formwork 1, and the piston 4 located in the funnel 2 can tightly fit into the loading opening 10 of the formwork 1 in this case, the cross-section and the size of the piston 4 are substantially equal or expediently somewhat smaller than the cross-section and the size of the loading opening 10 of the formwork 1.
    In the funnel 2 located above the formwork 1, a bell-shaped protective element 12 is provided with a hole directed to the lower side 13. The bell-shaped protective element 1.2 15 closes the guides 5, while its lower edge is in the region of the lower end of the vertically arranged guides 5. Bell-shaped protective element 12 is located at an equal distance 20 from the inner surface of the wall of the charging funnel 2 and from the outer surface of the guides 5, while its outer surface is appropriately curved, which facilitates 25 downward movement in the funnel 2 loaded in the direction of the arrow from the loose concrete mixture after the charging opening 10 ,
    The device includes a gas cylinder 14 containing COg gas under a pressure above atmospheric. The gas cylinder 14 is connected via a connecting line 15 containing shutoff valves to a discharge line 16, which is connected to a circulation gas pump 17. A supply line 18 is connected to the gas pump 17 from which branch lines 19-21 with valves 22-24 extend. Branched 40 pipelines 19-21 respectively enter the distribution chambers 25-27, which are located one above the other along the wall 8 of the formwork, with one of their limiting surfaces formed 45 by the outer side of the wall of the formwork itself. Chambers 25-27 are separated from one another (expediently gas-tight) by seals 28. Below chamber 29 - with a fitting 30 containing a valve for venting air and equalizing the gas pressure.
    Four chambers 3.1-34 are also attached to the outer surface of the wall 7 of the template. From chambers 31-33 pipelines 35-37 are taken off, each of which has a manometer 38 and a valve 39-41. Branch lines 35-37 are connected to a branch line 16, in which a vacuum pump 42 is integrated. In the lowermost chamber, there is a nipple 43 for venting air and equalizing the gas pressure with a valve 44 (check valve). Chambers 31-34 are also separated from one another by seals 28.
    > Through-holes 45 are provided in the walls 7 and 8 of the formwork (Fig. 2). In Fig. 1, these holes are indicated by a dash-and-dot line, Holes 45 allow gas to pass through the cavity 6 of the formwork and into chambers 25-27, 29 or chambers 31-34.
    Formwork 1 from top to bottom is divided into different sizes of technological zones I-IV, each of which includes a pair of chambers 25, 31,26, 32, 27, 33, 29, 34. The purpose of these zones will be explained below when describing the principle of operation of the proposed device according to invention.
    The gas supply into the cavity 6 of the formwork 1 can be produced not only by the method shown in Figs. 1 and 2, but also by means of the constructive solution shown in Figs. 3 and 4. In this case, the walls and 8 contain a system of channels made in accordance with with the aforementioned HV processing zones indicated in FIG. 1. The uppermost zone I includes two groups of holes, and zones II-IV - one group of meander-shaped holes 46 each, serving for gas passage. Holes 45 exit from the meander-shaped channel 47 and pass inside the wall of the formwork (for greater clarity, FIG. 3 shows only four holes 45 entering the cavity 6 of the formwork 1). Each gas distribution channel 47 has an outlet nozzle 48 connected to a pipeline 19-21 branching from the supply pipeline 18 (in the exemplary embodiment of the invention according to FIG. 3, considered here, to pipeline 19). Valves 22-24 are installed in each branch pipeline, so that the pressure of CO2 gas coming out of each group of holes 46 can be independently controlled. In the wall 7 of the formwork 1, a system of channels and holes can be provided (Fig. 3 and 4), and separate groups of holes are in communication with the branch pipes 35-37 from the discharge pipeline 16.
    Both in the exemplary embodiment according to FIGS. 1 and 2 of the chambers 31-34, and in the case of the exemplary embodiment according to FIGS. 3 and 4, the groups of holes 46 connected to independent gas pipelines allow the introduction of CO gas into the cavity 6 of the formwork 1 in locally defined zones with differing pressures from each other.
    Building panels are manufactured using the device according to Figs. 1 and 2 or Figs. 3 and 4 as follows.
    The hardening raw material mixture containing cement and fillers as a binder is uniformly and continuously fed into the funnel 2 according to the arrow c shown in FIG. 1. Subsequently hardening material (concrete mixture) moves down to the loading opening 10 of the formwork 1. The piston 4, moving reciprocally according to the double arrow b, makes about 15-300, but mostly 100-150 pressing movements per minute. The frequency of the reciprocating movements of the piston 4 can be varied (depending on the 'manufactured building element or the base material) over a wide range, for example, it can be moved at a very high speed. The bell-shaped protective element 12 is designed to prevent the ingress of the raw mixture of materials to the upper end of the guides 5, which would disrupt the operation of the piston 4 if it hit, or the loaded material would be pressed from the funnel 2 between the walls 7 and 8, that is, into the cavity 6 of the formwork 1 As a result of the compression of the mixture, due to relaxation, a multiple increase in its density occurs. The cavity 6 of the formwork 1 is filled with an amount of concrete mixture proportional to the lifting height of the piston 4, and the mixture is treated during its downward movement with COg gas (or a gas mixture containing COg gas), i.e. the carbonized cement-bound material leaves in a solidified state the outlet 11 of the formwork 1.
    The material moved by the piston 4 through the cavity 6 of the formwork 1 from top to bottom is processed in the technological zones I-IV, while the carbonization is carried out mainly in the zones I-III.
    In the uppermost zone 1, in the area of the loading opening 10, a gas-tight layer is formed therein by compaction of the concrete mixture, i.e. mechanically using the forces of relaxation of the compressed material, they prevent the leakage of CO2 gas through the chamber 25 and holes 45 introduced into the cavity 6 of the formwork 1. Since the raw mixture of materials is continuously loaded and compacted with a rammer, it also exists in the upper part of the formwork throughout the entire process production, in some way, a gas-tight core, that is, it seems to be reduced all the time. The action of the mechanical seal extends over the entire section 1 (although weakening from top to bottom). Since the relaxation force is significant, in order to introduce COg gas into the pores of the raw material mixture, a rather large excess gas pressure and / or the use of vacuum on the side of the wall 7 are required. Gas COg must be pressed into the pores of the material mixture. The required gas pressure, for example 6 bar, can be set using valve 22 (see figure 1). The efficiency of introducing CO gas into the mixture of materials can be increased by a vacuum pump 42 (with valve 39 open). A pressure gauge 38 built into the pipeline 35 makes it possible to control the pressure of the flowing gas, and the valves 22 and 39 are activated if necessary. Applying a vacuum, for example, 0.5 bar, a pressure difference is created on the inner surface of plates 7 and 8 in the formwork 1, due to which there is a clearly greater intensification of the transverse gas flow directed from the wall 8 to the wall 7 of the formwork and the pores of the material mixture are uniformly filled with CO2 gas along the entire cross section.
    In zone 1, the pores of the material mixture are filled with gas, and the excess gas entering through the holes 45 of the walls 8 of the formwork into the chamber 31 with a lower pressure (for example, 3 bar) enters through the line 35 and the line 16 back into the gas circulation loop. However, figure 1 shows an arrow of the direction of gas flows in pipelines. The path of the gas entering from the branch line 19 into the chamber 25 is shown in Fig. 2 by an arrow e, and the path of the gas entering through the holes 45 into the cavity 6 of the formwork is indicated by the arrows f. Positions e and f in Fig. 3 and 4 have the indicated meanings. Here you should pay attention to the fact that according to the solution of introducing gas, shown in Fig. 3 and 4, it is sufficient to introduce it into the cavity 6 of the formwork through the second group of holes 46 (see Fig. 3) with a lower pressure equal, for example, 5 bar e the lower section of zone 1, where the sealing effect of piston 4 is less pronounced and therefore the material has a lower density (the internal stress of the compressed mixture is greatest at the end of zone 1 and gradually decreases from top to bottom). In this case, the outgoing residual gas has a pressure of about 2-3 bar. The pressure 5 of COg gas introduced into zone 1 must be selected so that gas does not leak through the sealing layer of the mixture of materials in the area of the loading opening of the formwork 1, which is above zone 1.
    Since the gas-tight state is also ensured between the inner surfaces of the walls 7 and 8 of the formwork 1 and the mixture of materials, leakage of CO gas is also prevented from the cavity 6 of the formwork 15 along the walls. When a gas with two different pressures is introduced, it cannot penetrate from the bottom up towards the opening 10, as this is prevented by the high-pressure gas, the latter pushing 20 the gas with a lower pressure towards the opposite wall 7, that is, forcing it to penetrate the mixture of materials in the transverse direction.
    In zone 1, the chemical reaction between CO2 gas and cement, i.e. carbonation is just beginning, but in zone 11 it proceeds explosively (instant reaction). In this chemical reaction, the absorption of CO 2 introduced into zone 1 occurs and, as a consequence of this, a drop in pressure occurs, while if additional CO 2 gas were not introduced, then a vacuum would form in the mixture of materials. In section 11, therefore, continue to be introduced through the branch pipeline
    20 and chamber 26 COg gas and thus recover in zone 1 the COg gas consumed in the carbonization reaction. CO2 gas is introduced into the zone with a lower pressure, but still higher than atmospheric pressure, for example, with a pressure of 4 bar, because there is no need to introduce a high pressure gas into the pores of a mixture of materials, since the gas, passing through the material, enters the chamber 32 with a pressure of about 45 bar, and from there it is returned back to the gas circulation through the branch line 36 and the outlet line 16. The valve 40 can also be used to use vacuum in zone 11, but this is not considered necessary.
    The hardening of the mixture of materials begins to a lesser extent already in zone 1 and it reaches such an extent in zone 11 that the action of the relaxation force completely ceases. The building panel 9, which is in the hardening phase (see Fig. 1), can freely and continuously move downward in the formwork 1, since the material does not exert pressure on the walls of the formwork, as in the upper part of zone 1, where, under the pressing pressure of the piston 4, it still moves downwards not hardened - Ί mixture of materials. As a result of the chemical reaction of carbonization, a vacuum is formed in the material. five
    The pressure of the CO2 gas introduced into zone III continues to drop, since gas is introduced here at a pressure of, for example, 1 bar. In this zone, the carbonization process is almost completely completed. The amount of gas introduced into zone III-10 must cover the still existing demand for gas necessary for the complete completion of the carbonation reaction. The loss of CO2 gas at the lower end of the cavity 6 of the formwork 1, i.e. at the outlet 15, nozzle 11, from which the compressed, carbonized and partially solidified material comes out, can be prevented by setting appropriate pressure conditions in zone III - by introducing into this zone a minimum amount of COg gas with a minimum pressure. The pressure of the residual CO2 gas entering the chamber 33, if there is no vacuum, is not much lower than the pressure of the supplied gas, for example, 0.8-0.9 bar. Thus, the carbonation reaction is reliably completed. In zones II and III, a pump 42 can create a vacuum in chambers 32 and 33, equal to, for example, 0.5 bar, in order to intensify the gas flow 30 in the transverse direction.
    Zone IV is a compensation zone, into which CO2 gas is no longer injected. In this zone, practically no 35 chemical reaction occurs. In chambers 31 and 34, along the inner surface of plates 7 and 8, possibly flowing COg gas from the inside to the outside enters, while its amount or its pressure in zone 111 is selected so that 40 gas is sufficient there to complete the carbonization reaction. Gas can be released through the control valves 44 and the union 43 and the union 30 if the COg gas pressure in zone III is correctly selected. Hence. 45 with the help of these control valves of connection 43 and connection 30 it is possible to equalize the pressure of CO gas in zone IV,
    If, for the chemical reaction of carbonization, not pure gas of 50 COg is used, but a gas mixture that contains not only COg gas (for example, in an amount of 30%), then the neutral components of this mixture will not be consumed during the carbonization reaction. Since in this case the amount of gas (amount of air) leaving through the control valves of the fittings 43 and 30 can be quite large, these control valves act as air valves!
    Although the carbonization phases are separated from one another both spatially and temporally, the whole carbonization process is continuous, because the material formed into the hardening building panels continuously passes through the cavity 5 of the formwork. The building panel 9 extending continuously through the outlet is cut with a crosscut circular saw 49 (see FIG. 1) to a specified length. The circular saw 49 operates synchronously with the speed of the compressed material coming out and therefore obtains already partially hardened building panels (having about 30% 28-day durability), which finally harden when artificially applied to them in a traditional way or naturally.
    The cross-sectional shape of the building panel 9 made with this device is shown in Fig. 6, but it is easy to understand that with this device it is possible to produce (within practical limits) building elements with any cross-sectional shape, choosing for this purpose the corresponding cross-sectional shape. section of the piston of the th template. The building element 50 (Fig. 7) is made with a wedge-shaped cross-section, and the building element 51 (Fig. 8) has a wavy shape. Figure 9 shows a building element 52 with a trapezoidal profile. It goes without saying that hollow bodies can also be produced with the inventive device. Shown in FIG. 10, the building element 53 is circular in cross-section with an internal cavity. 11 shows a building element 54 with a rectangular cross-sectional shape with internal cavities 55 and 56. For the manufacture of a hollow building element, special formwork templates must be used. Fig. 12 shows a formwork structure for manufacturing the building elements shown in Fig. 11. In the outer frame of the template 57, in the walls of the inner cores 58 and 59 with voids 60 and 61, channels are located, similar to, for example, the channels in FIGS. 3 and 4 for introducing CO2 gas and passing it through the material moving in the template. The gas flow is indicated in FIG. 12 by arrows, while the channels and holes are not shown for clarity.
    The amount of CO2 gas required for the carbonization reaction is always proportional to the amount of cement used for a given recipe and constitutes about 8-10 wt% of the amount of cement. It is advisable that the gas mixture used for carbonization, since no pure COg gas is used, should contain at least 30% COg gas.
    PRI me R 1. According to the method according to the invention, using the device shown in FIGS. 1 and 2, building panels with a size of 60x100 cm and a thickness of 20 mm are produced. The composition of the crude mixture intended for formation by compression and hardening during carbonization treatment is as follows, wt%:
    Cement 42 Slaked lime 2 Quartz sand 42 Water fourteen Introduction of CO2 gas into the moving
    down in the formwork 1, the material is produced in the NI zones, i.e. from top to bottom, with the following pressures:
    zone I: inlet bbar zone III: inlet 0.4 bar outlet 3 bar outlet about 0 zone II: inlet 2 bar outlet 1 bar
    In compensation zone IV, gas possibly escaping from zone III downwardly is released along the inner surfaces of the formwork walls. Here we can only talk about the minimum amount of gas.
    The material moves through the cavity 6 of the formwork at a speed of 1 m per minute.
    From the gas pressure-path-time diagram (see Fig. 5), in which the letter V denotes the speed of the material moving down through the formwork, P o is the density of the hardening mixture of materials, d is the thickness of the manufactured building panel, it follows that the material passes through zone 1, where the CO2 gas pressure is highest (6 bar) in about 2 minutes, while the passage of zones 11 and III generally requires about a minute, while the gas pressure decreases gradually to zero and in zone IV the gas no longer has an excess pressure. The curve in Fig. 5 characterizes the internal relaxation force, which is proportional to the compression force generated by the piston, or the force required for the pressing process, that is, for compaction and further movement of the pressed material, always proportional to the relaxation force acting on the side walls of the formwork.
    The flexural strength of the material exiting through the outlet 11 of the formwork 1 is about 35 kg / cm 2 , i.e. about 30% of the final 28-day strength, and the density is 1250 kg / cm 3 . Using a circular saw, the panel material continuously emerging from the formwork is cut to a certain length. The panels, partially hardened by carbonation, are placed on the edge for further storage.
    PRI me R 2. According to the method according to the invention, using the device shown in FIGS. 1, 2 and 3, building elements with a size of 163x1250x4000 mm and a wall thickness of 14 mm are produced, containing cavities. The composition of the molded, processed carbonization hardening mixture of materials next, May. %:
    Cement 58 Dissolving glass 1 Wood shavings fourteen Water 24
    Slaked lime 3
    The raw mixture of materials with the composition indicated in this example is pressed into the formwork 1 by alternating movements of the piston 4 of the device according to Figs. 1 and 2. In the area of the loading opening 10 of the cavity 6 of the formwork 1, the same maximum internal stress is provided until the piston 4 continuously compresses the material. Thus, as a result of the mechanical seal, a gas-tight state is guaranteed during the entire manufacturing process of the building element.
    The pressure of the gas introduced into and out of the NI zones is equal to the pressure according to example 1, and the gas pressure-path-time diagram is similar to the diagram in Fig. 5, however, the volumetric weight and strength of the final product are lower due to different fillers.
    权利要求:
    Claims (4)
    [1]
    Claim
    1. A method for the manufacture of construction products based on cement and / or lime, including the supply of concrete mixture to the formwork, its compaction, supply of CO2 under pressure and evacuation, stripping and hardening, characterized in that, in order to increase productivity, the concrete mixture is fed continuously into the vertical formwork, the compaction is carried out by ramming, and in the course of moving the concrete mixture downwards, COg is fed from one side with a decrease in pressure along the zones, and COg is removed from the opposite side.
    [2]
    2, The method according to claim 1, with the fact that the CO2 supply pressure is reduced by zone according to the following mode: in zone I, 3-5 bar; in zone II 2-3 bar: in 111 1-2 bar: in zone IV CO2 extraction.
    [3]
    3. The method according to claims 1 and 2. is characterized by the fact that the supply of CO 2 is carried out in a mixture of gases with a CO 2 content of 30-99%.
    ,4. The method according to claims 1 to 3, characterized in that the removal of CO 2 is carried out by evacuation.
    5. A device for the manufacture of building products, containing a loading funnel connected to the forming through vertical formwork, placed in the loading funnel, a compaction ramming mechanism installed with the possibility of reciprocating movement along the guides and equipped with a bell-shaped protective element, characterized in that, for the purpose increasing productivity when using a CO 2 hardening accelerator, the device is equipped with a system for supplying CO 2 and removing it, and the parallel walls of the formwork are made with opposed holes for supplying and removing CO 2 with the formation of autonomous zones HV, while the walls of the formwork cn-zZ are shielded divided into cameras corresponding to zones 1-IV.
    6. The device according to claim 5, characterized in that the CO 2 supply and removal system comprises a gas pump and a supply pipeline connected on one side with a gas cylinder, and on the other with zonal pipelines communicated through the casing chambers with holes in formwork walls of zones ll II.
    7. A device according to claims 5 and 6, characterized by the fact that, in order to ensure a local supply of CO 2 , the walls of the formwork are made with groups of additional holes arranged to form meander-shaped channels, each of which is connected, respectively, with the zonal pipeline and with outlet zonal pipeline.
    fig / .i '
    View B e 4> c
    44 - ^ - 4-4-4-4 * Z
    40 e * 4 - 0-4 - f— G * "—O ~" Q—
    0-4-4 - ^ / ___J in - 4-4 ·
    Fie.4
    [4]
    4 M (pml ν
    Ro * 4200 g / = b! = DODM /
    3 D ... ————-- .- 4GcKbelTandtiingszeit
    2 = 1
    3 '.
    ------------ l · ----------- 1—
    3, 'C
    -Η -——- g — γr ~
    LOU E zones /
    Press! reck εη lc ng efZbnen)
    Fig. 5
    FIG. eleven
    类似技术:
    公开号 | 公开日 | 专利标题
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    同族专利:
    公开号 | 公开日
    YU45499B|1992-05-28|
    EP0290007A1|1988-11-09|
    HU199363B|1990-02-28|
    FI88285C|1993-04-26|
    FI882080A|1988-11-06|
    JPS63290709A|1988-11-28|
    YU86788A|1990-02-28|
    US4927573A|1990-05-22|
    IN169499B|1991-10-26|
    EP0290007B1|1991-08-21|
    FI882080A0|1988-05-04|
    NZ224370A|1991-05-28|
    DD268661A5|1989-06-07|
    FI88285B|1993-01-15|
    AU1523688A|1988-11-10|
    AU602764B2|1990-10-25|
    AT66444T|1991-09-15|
    DE3864307D1|1991-09-26|
    US4917587A|1990-04-17|
    YU92389A|1992-07-20|
    JPH0639087B2|1994-05-25|
    US5051217A|1991-09-24|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    HU872004A|HU199363B|1987-05-05|1987-05-05|Process for production and equipment for elements especially constructing elements from afterhardening materials|
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